CN105561696B - Gas-liquid separator for desulfurization dust-removal system - Google Patents
Gas-liquid separator for desulfurization dust-removal system Download PDFInfo
- Publication number
- CN105561696B CN105561696B CN201510666043.8A CN201510666043A CN105561696B CN 105561696 B CN105561696 B CN 105561696B CN 201510666043 A CN201510666043 A CN 201510666043A CN 105561696 B CN105561696 B CN 105561696B
- Authority
- CN
- China
- Prior art keywords
- escape pipe
- gas
- liquid separator
- web plate
- isocon
- Prior art date
- Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
- Expired - Fee Related
Links
- 239000007788 liquid Substances 0.000 title claims abstract description 35
- 238000006477 desulfuration reaction Methods 0.000 title claims abstract description 18
- 230000023556 desulfurization Effects 0.000 title claims abstract description 18
- 235000008733 Citrus aurantifolia Nutrition 0.000 claims abstract description 26
- 235000011941 Tilia x europaea Nutrition 0.000 claims abstract description 26
- 239000004571 lime Substances 0.000 claims abstract description 26
- 241000883990 Flabellum Species 0.000 claims description 7
- 230000015572 biosynthetic process Effects 0.000 claims 1
- 238000010276 construction Methods 0.000 abstract description 4
- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 abstract description 4
- 239000007789 gas Substances 0.000 description 10
- 238000000926 separation method Methods 0.000 description 3
- 230000003009 desulfurizing effect Effects 0.000 description 2
- 239000000203 mixture Substances 0.000 description 2
- 239000002912 waste gas Substances 0.000 description 2
- UCKMPCXJQFINFW-UHFFFAOYSA-N Sulphide Chemical compound [S-2] UCKMPCXJQFINFW-UHFFFAOYSA-N 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 230000006378 damage Effects 0.000 description 1
- 230000000694 effects Effects 0.000 description 1
- 238000005516 engineering process Methods 0.000 description 1
- 238000000605 extraction Methods 0.000 description 1
- 238000009776 industrial production Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 239000000126 substance Substances 0.000 description 1
- 238000006467 substitution reaction Methods 0.000 description 1
- 235000020681 well water Nutrition 0.000 description 1
- 239000002349 well water Substances 0.000 description 1
Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D45/00—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces
- B01D45/04—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia
- B01D45/08—Separating dispersed particles from gases or vapours by gravity, inertia, or centrifugal forces by utilising inertia by impingement against baffle separators
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D53/00—Separation of gases or vapours; Recovering vapours of volatile solvents from gases; Chemical or biological purification of waste gases, e.g. engine exhaust gases, smoke, fumes, flue gases, aerosols
- B01D53/26—Drying gases or vapours
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D2257/00—Components to be removed
- B01D2257/80—Water
Abstract
The present invention provides a kind of gas-liquid separator for desulfurization dust-removal system, including air inlet pipe, isocon, escape pipe；The air inlet pipe draws the uniform isocon of two axisymmetricals on air inlet pipe；The outflow end of each isocon is facing each other, and vertical connection makes two isocons form doab in escape pipe in the both sides of the escape pipe；There is the central lime set web plate for being right against two isocons in the doab；And the both ends of the escape pipe are also opened respectively end lime set web plate.The gas-liquid separator not only has good water rem oval, and simple in construction, and cost is relatively low.
Description
Technical field
The present invention relates to field of environment protection equipment, is a kind of gas-liquid separator for desulfurization dust-removal system especially.
Background technology
In field of industrial production, for waste gas caused by the equipment such as boiler, more sulfide is usually contained, in order to prevent
Pollution to air, it is necessary to handled by desulfurization dust-removal system waste gas, usually, the system includes deduster, desulfurization
Tower, and three big core of gas-liquid separation device.Wherein, desulfurizing tower mainly carries out desulfurization by the way of aqueous slkali is sprayed,
Therefore, a large amount of moisture content are contained from the gas of desulfurizing tower discharge, if do not carried out gas-liquid separation to it, then this kind includes chemical substance
Liquid will cause larger destruction to external environment；Therefore, in current system, generally using corrugated plate type gas-liquid separator or
Centrifugal gas-liquid separator；Wherein, corrugated plate type gas-liquid separator enters mainly by the folded walls on wave-shape board to gas-liquid mixture
Row stops that, so as to be collected to liquid, its water removal effect is poor naturally；And for centrifugal gas-liquid separator, then need to match somebody with somebody
The spiral fan mechanism of heavy-duty motor and complexity is put, cost is larger.
The content of the invention
In view of the above-mentioned problems, it is an object of the invention to provide a kind of gas-liquid separator for desulfurization dust-removal system, gas
Liquid/gas separator not only has good water rem oval, and simple in construction, and cost is relatively low.
Technical scheme is used by the present invention realizes technical purpose：This is used for the gas-liquid separator bag of desulfurization dust-removal system
Include air inlet pipe, isocon, escape pipe；The air inlet pipe draws the uniform shunting of two axisymmetricals on air inlet pipe
Pipe；The outflow end of each isocon is facing each other, and vertical connection makes two isocons exist in the both sides of the escape pipe
Doab is formed in escape pipe；There is the central lime set web plate for being right against two isocons in the doab；It is and described
The both ends of escape pipe are also opened respectively end lime set web plate.
Preferably, the central lime set web plate is on the axis of the escape pipe.
Preferably, the total cross-sectional area of two described isocons is less than the cross-sectional area of the air inlet pipe, so that point
Higher air pressure is kept in flow tube.
Preferably, the part on the central lime set web plate above isocon is downward opening with more than one piece
Chev(e)ron baffle, so that the drop being condensed on central lime set web plate can not migrate upwards under the traction of air-flow, can only be downward
Drippage, in order to collect.
Preferably, two described isocons are concatenating a rotating shaft at the escape pipe respectively, make it is described go out
Tracheae can be rotated freely around the axis of two isocons, and one and the escape pipe geo-stationary are provided with the rotating shaft
Flabellum, and two flabellums are symmetrical on the escape pipe；An arc is provided with the Plane of rotation of the escape pipe
Guide housing, the arcuate guide cover it is opening down.
The beneficial effects of the present invention are：This is used for the gas-liquid separator of desulfurization dust-removal system at work, by air inlet pipe
After the high moisture content gas flowed into is via symmetrical isocon shunting, when confluxing, mutually head-on collision, so that river outlet air pressure
Drastically raise, gas liquefaction ability is risen sharply, and the river outlet arranges the central lime set web plate, provides to form field for drop
Institute；Moisture content in gas can thus largely condensed on central lime set web plate；It can be seen that the gas-liquid separator not only has well
Water rem oval, and simple in construction, cost is relatively low.
Brief description of the drawings
Fig. 1 is this elevational schematic for the gas-liquid separator embodiment one of desulfurization dust-removal system.
Fig. 2 is this elevational schematic for the gas-liquid separator embodiment two of desulfurization dust-removal system.
Embodiment
The present invention is further described with reference to the accompanying drawings and examples：
In the embodiment one shown in Fig. 1, the gas-liquid separator for being used for desulfurization dust-removal system includes air inlet pipe 1, shunting
Pipe 21,22, escape pipe 3；The uniform isocon 21 of two axisymmetricals on air inlet pipe 1 of the extraction of air inlet pipe 1,
22；The outflow end of each isocon 21,22 is facing each other, and vertical connection makes this two pieces points in the both sides of the escape pipe 3
Flow tube 21,22 forms doab in escape pipe 3；Have in the doab and be right against in two isocons 21,22
Entreat lime set web plate 4；And the both ends of the escape pipe 3 are also opened respectively end lime set web plate 5.
Above-mentioned gas-liquid separator, the central lime set web plate 4 are herein gas on the axis of the escape pipe 3
The center that stream liquidates, there is maximum air pressure, therefore most useful for lime set.
Above-mentioned gas-liquid separator, the total cross-sectional area of described two isocons 21,22 are less than the horizontal stroke of the air inlet pipe 1
Sectional area, so as to keep higher air pressure in isocon 21,22.
In addition, the part on the central lime set web plate 4 above the doab has the downward opening people of polylith
Font baffle plate 6, so that the drop being condensed on central lime set web plate 4 can not migrate upwards under the traction of air-flow, can only be downward
Drippage, in order to collect.
At work, the high moisture content gas flowed into by air inlet pipe 1 passes through the above-mentioned gas-liquid separator for desulfurization dust-removal system
After being shunted by symmetrical isocon 21,22, when confluxing, mutually head-on collision, so that river outlet air pressure drastically raises, make gas
Body liquefying power rises sharply, and the river outlet arranges the central lime set web plate 4, provides to form place for drop；Thus can make
Moisture content in gas largely condenses on central lime set web plate 4；It can be seen that the gas-liquid separator not only there is good water removal to imitate
Rate, and it is simple in construction, and cost is relatively low.
For the embodiment two shown in Fig. 2, it is with the difference of embodiment one：Described two isocons 21,22
A rotating shaft 210,220 is being concatenated respectively at the escape pipe 3, make the escape pipe 3 can around two isocons 21,
The axis of 22 outflow end is rotated freely, and a fan with the geo-stationary of escape pipe 3 is provided with the rotating shaft 210,220
Leaf, and two flabellums are symmetrical on the escape pipe 3；Specifically, two rotating shafts 210, point of 220 outer ends can be made
Flow tube 21,22 is fixed on the outer ring of rotating shaft, and makes two rotating shaft 210,220 inner（I.e. close to one end of escape pipe 3）It is fixedly connected
In escape pipe 3；An arcuate guide cover 7, the opening court of the arcuate guide cover 7 are provided with the Plane of rotation of the escape pipe 3
Under.In addition, in embodiment two, the chev(e)ron baffle 6 in embodiment one is no longer set.
According to the scheme of embodiment two, isocon 21,22 during escape pipe 3 is flowed to, promote the bearing 210,
Flabellum in 220 is quickly rotated, and so as to drive the escape pipe 3 to rotate, during being somebody's turn to do, flabellum is formed to the air-flow in isocon
Larger resistance, the air pressure in isocon is significantly improved, so that drop just has started to largely be formed in isocon, work as gas-liquid
After mixture passes through bearing, pressure is released, and forms quick vapour-liquid stream, condenses a large amount of liquid on the central lime set web plate 4
Body, also, due to the quick rotation of escape pipe 3, the liquid at the central center of lime set web plate 4 is quickly excluded to the periphery, make center
The center of lime set web plate 4 remains optimal lime set condition, so as to further increase gas-liquid separation ability.
The foregoing is only presently preferred embodiments of the present invention, be not intended to limit the invention, it is all the present invention spirit and
Within principle, any modification, equivalent substitution and improvements made etc., it should be included in the scope of the protection.
Claims (4)
1. a kind of gas-liquid separator for desulfurization dust-removal system, including air inlet pipe（1）, isocon（21、22）, escape pipe（3）；
The air inlet pipe（1）Two are drawn on air inlet pipe（1）The uniform isocon of axisymmetrical（21、22）；Each described point
Flow tube（21、22）Outflow end it is facing each other, and vertical connection is in the escape pipe（3）Both sides, make two isocons
（21、22）In escape pipe（3）Interior formation doab；Have in the doab and be right against two isocons（21、22）'s
Central lime set web plate（4）；And the escape pipe（3）Both ends also open respectively and have end lime set web plate（5）;It is characterized in that：Institute
Two isocons stated（21、22）Close to the escape pipe（3）Place concatenates a rotating shaft respectively（210、220）, make it is described go out
Tracheae（3）Can be around two isocons（21、22）Axis rotate freely, the rotating shaft（210、220）Inside be provided with one with
The escape pipe（3）The flabellum of geo-stationary, and two flabellums are on the escape pipe（3）Symmetrically；The outlet
Pipe（3）Plane of rotation in be provided with an arcuate guide cover（7）, the arcuate guide cover（7）It is opening down.
2. the gas-liquid separator according to claim 1 for desulfurization dust-removal system, it is characterised in that：The central lime set
Web plate（4）Located at the escape pipe（3）Axis on.
3. the gas-liquid separator according to claim 1 or 2 for desulfurization dust-removal system, it is characterised in that：Described two
Root isocon（21、22）Total cross-sectional area be less than the air inlet pipe（1）Cross-sectional area.
4. the gas-liquid separator according to claim 1 or 2 for desulfurization dust-removal system, it is characterised in that：The center
Lime set web plate（4）It is upper to be in isocon（21、22）The part of top has more than one piece downward opening chev(e)ron baffle（6）,
So as to it is condensed in central lime set web plate（4）On drop can not be migrated upwards under the traction of air-flow, can only drip downwards.
Priority Applications (2)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510666043.8A CN105561696B (en) | 2015-10-16 | 2015-10-16 | Gas-liquid separator for desulfurization dust-removal system |
| CN201710971794.XA CN107510994B (en) | 2015-10-16 | 2015-10-16 | A kind of working method of the gas-liquid separator for desulfurization dust-removal system |
Applications Claiming Priority (1)
| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201510666043.8A CN105561696B (en) | 2015-10-16 | 2015-10-16 | Gas-liquid separator for desulfurization dust-removal system |
Related Child Applications (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710971794.XA Division CN107510994B (en) | 2015-10-16 | 2015-10-16 | A kind of working method of the gas-liquid separator for desulfurization dust-removal system |
Publications (2)
| Publication Number | Publication Date |
|---|---|
| CN105561696A CN105561696A (en) | 2016-05-11 |
| CN105561696B true CN105561696B (en) | 2017-11-24 |
Family
ID=55872661
Family Applications (2)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710971794.XA Active CN107510994B (en) | 2015-10-16 | 2015-10-16 | A kind of working method of the gas-liquid separator for desulfurization dust-removal system |
| CN201510666043.8A Expired - Fee Related CN105561696B (en) | 2015-10-16 | 2015-10-16 | Gas-liquid separator for desulfurization dust-removal system |
Family Applications Before (1)
| Application Number | Title | Priority Date | Filing Date |
|---|---|---|---|
| CN201710971794.XA Active CN107510994B (en) | 2015-10-16 | 2015-10-16 | A kind of working method of the gas-liquid separator for desulfurization dust-removal system |
Country Status (1)
| Country | Link |
|---|---|
| CN (2) | CN107510994B (en) |
Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102049149A (en) * | 2009-10-27 | 2011-05-11 | 中国石油化工股份有限公司 | Tower feeding distributor |
| CN104258642A (en) * | 2014-10-13 | 2015-01-07 | 四川省德阳升发石油工具有限公司 | Natural gas filter |
Family Cites Families (5)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| US8151460B2 (en) * | 2007-01-30 | 2012-04-10 | Intek, Inc. | Heat exchanger deep bundle air extractor and method for modifying |
| US20080257163A1 (en) * | 2007-04-19 | 2008-10-23 | Big Bang Co., Ltd | Gas-liquid separator, exhaust cleaner or air cleaner using the separator, and sterilizing air cleaner |
| US7901485B2 (en) * | 2007-07-11 | 2011-03-08 | Mccutchen Co. | Radial counterflow carbon capture and flue gas scrubbing |
| EP2463008A1 (en) * | 2010-12-10 | 2012-06-13 | NTNU Technology Transfer AS | A separator for separating a fluid flow of gas with a dispersed phase |
| CN204134375U (en) * | 2014-08-15 | 2015-02-04 | 北京日新达能技术有限公司 | A kind of composite efficient separator-combination demister |
-
2015
- 2015-10-16 CN CN201710971794.XA patent/CN107510994B/en active Active
- 2015-10-16 CN CN201510666043.8A patent/CN105561696B/en not_active Expired - Fee Related
Patent Citations (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN102049149A (en) * | 2009-10-27 | 2011-05-11 | 中国石油化工股份有限公司 | Tower feeding distributor |
| CN104258642A (en) * | 2014-10-13 | 2015-01-07 | 四川省德阳升发石油工具有限公司 | Natural gas filter |
Also Published As
| Publication number | Publication date |
|---|---|
| CN107510994A (en) | 2017-12-26 |
| CN107510994B (en) | 2019-06-11 |
| CN105561696A (en) | 2016-05-11 |
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Legal Events
| Date | Code | Title | Description |
|---|---|---|---|
| C06 | Publication | ||
| PB01 | Publication | ||
| C10 | Entry into substantive examination | ||
| SE01 | Entry into force of request for substantive examination | ||
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20170915 Address after: 362100, Luohe Road, 92 Town, Luoyang Town, Huian County, Fujian, Quanzhou Applicant after: Wu Zhenbiao Address before: 210000 Jiangsu city of Suzhou province Xiangcheng District Guangji road building 89 Room 201 garden homes Applicant before: Hu Zhenqiang |
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| CB02 | Change of applicant information | ||
| CB02 | Change of applicant information |
Address after: 362100, Luohe Road, town, Luoyang Town, Quanzhou, Quanzhou, Fujian Applicant after: Wu Zhenbiao Address before: 362100, Luohe Road, 92 Town, Luoyang Town, Huian County, Fujian, Quanzhou Applicant before: Wu Zhenbiao |
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| TA01 | Transfer of patent application right |
Effective date of registration: 20171012 Address after: Nanshan Road, Jiahua building of Quangang District of Quanzhou City, Fujian Province, No. 90 362800 Applicant after: Quanzhou Runmei Quangang Environmental Protection Technology Co. Ltd Address before: 362100, Luohe Road, town, Luoyang Town, Quanzhou, Quanzhou, Fujian Applicant before: Wu Zhenbiao |
|
| TA01 | Transfer of patent application right | ||
| CB03 | Change of inventor or designer information | ||
| CB03 | Change of inventor or designer information |
Inventor after: Chen Guojun Inventor after: Wu Handong Inventor before: Hu Zhenqiang |
|
| TA01 | Transfer of patent application right | ||
| TA01 | Transfer of patent application right |
Effective date of registration: 20171024 Address after: 242100 Zhong Meilu, Langxi Economic Development Zone, Xuancheng, Anhui Applicant after: Anhui Zhong Hao environmental protection equipment Limited by Share Ltd Address before: Nanshan Road, Jiahua building of Quangang District of Quanzhou City, Fujian Province, No. 90 362800 Applicant before: Quanzhou Runmei Quangang Environmental Protection Technology Co. Ltd |
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| GR01 | Patent grant | ||
| GR01 | Patent grant | ||
| CF01 | Termination of patent right due to non-payment of annual fee | ||
| CF01 | Termination of patent right due to non-payment of annual fee |
Granted publication date: 20171124 Termination date: 20201016 |